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公开(公告)号：US08513314B2
公开(公告)日：2013-08-20
申请号：US12863011
申请日：2009-02-12
Applicant: Max Thorhauge
Inventor： Max Thorhauge
IPC: C07C27/00
CPC classification number: B01J8/0285 , B01J8/009 , B01J8/0214 , B01J8/0292 , B01J8/067 , B01J2208/00115 , B01J2208/00123 , B01J2208/00132 , B01J2208/0015 , B01J2208/00212 , B01J2219/00772 , C07C29/152 , Y02P20/52 , C07C31/04
Abstract: Improved design of a catalytic reactor for the production of methanol at equilibrium conditions whereby methanol as it is formed is separated from the gaseous phase into the liquid phase within the reactor, without reducing the catalytic activity of the methanol catalysts This is achieved by adjusting the boiling point of a liquid cooling agent being in indirect contact with the catalyst particles and by providing a specific ratio of catalyst bed volume to cooling surface area. Thereby, condensation of methanol as it is formed in the gaseous phase takes place at the cooling surface arranged evenly distributed within the reactor and within a very limited region of the catalyst bed.
Abstract translation: 用于在平衡条件下生产甲醇的催化反应器的改进设计，其中形成的甲醇在反应器内从气相分离成液相，而不降低甲醇催化剂的催化活性。这通过调节沸点 液体冷却剂的点与催化剂颗粒间接接触，并且通过提供催化剂床体积与冷却表面积的特定比例。 因此，在气相中形成的甲醇的冷凝发生在均匀分布在反应器内并且在催化剂床的非常有限的区域内的冷却表面上。
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公开(公告)号：US08202915B2
公开(公告)日：2012-06-19
申请号：US12812480
申请日：2009-02-12
Applicant: Max Thorhauge
Inventor： Max Thorhauge
IPC: C07C27/00
CPC classification number: B01J8/0285 , B01J8/009 , B01J8/0214 , B01J8/0292 , B01J8/067 , B01J2208/00115 , B01J2208/00123 , B01J2208/00132 , B01J2208/0015 , B01J2208/00212 , B01J2219/00772 , C07C29/152 , Y02P20/52 , C07C31/04
Abstract: Improved design of a catalytic method and reactor for the production of methanol at equilibrium conditions whereby methanol as it is formed is separated from the gaseous phase into the liquid phase within the reactor without reducing the catalytic activity of the methanol catalyst. This is achieved by adjusting the boiling point or temperature of a liquid cooling agent being in indirect contact with the catalyst particles and by providing a specific ratio of catalyst bed volume to cooling surface area. Thereby, condensation of methanol as it is formed in the gaseous phase takes place for the most at the cooling surface arranged evenly distributed within the reactor and if at all within a very limited region of the catalyst bed.
Abstract translation: 用于在平衡条件下生产甲醇的催化方法和反应器的改进设计，其中形成的甲醇在反应器内从气相分离成液相而不降低甲醇催化剂的催化活性。 这是通过调节与催化剂颗粒间接接触的液体冷却剂的沸点或温度，并通过提供催化剂床体积与冷却表面积的特定比例来实现的。 因此，在气相中形成的甲醇的冷凝最多发生在均匀分布在反应器内的冷却表面，如果完全在催化剂床的非常有限的区域内。
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公开(公告)号：US20100305222A1
公开(公告)日：2010-12-02
申请号：US12812480
申请日：2009-02-12
Applicant: Max Thorhauge
Inventor： Max Thorhauge
CPC classification number: B01J8/0285 , B01J8/009 , B01J8/0214 , B01J8/0292 , B01J8/067 , B01J2208/00115 , B01J2208/00123 , B01J2208/00132 , B01J2208/0015 , B01J2208/00212 , B01J2219/00772 , C07C29/152 , Y02P20/52 , C07C31/04
Abstract: Improved design of a catalytic method and reactor for the production of methanol at equilibrium conditions whereby methanol as it is formed is separated from the gaseous phase into the liquid phase within the reactor without reducing the catalytic activity of the methanol catalyst. This is achieved by adjusting the boiling point or temperature of a liquid cooling agent being in indirect contact with the catalyst particles and by providing a specific ratio of catalyst bed volume to cooling surface area. Thereby, condensation of methanol as it is formed in the gaseous phase takes place for the most at the cooling surface arranged evenly distributed within the reactor and if at all within a very limited region of the catalyst bed.
Abstract translation: 用于在平衡条件下生产甲醇的催化方法和反应器的改进设计，其中形成的甲醇在反应器内从气相分离成液相而不降低甲醇催化剂的催化活性。 这是通过调节与催化剂颗粒间接接触的液体冷却剂的沸点或温度，并通过提供催化剂床体积与冷却表面积的特定比例来实现的。 因此，在气相中形成的甲醇的冷凝最多发生在均匀分布在反应器内的冷却表面，如果完全在催化剂床的非常有限的区域内。
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公开(公告)号：US07138094B2
公开(公告)日：2006-11-21
申请号：US10352024
申请日：2003-01-28
Applicant: Haldor F. A. Topsøe , Hans Jensen-Holm , Ole Ekner , Søren Selde Enevoldsen , Max Thorhauge , Per Morsing
Inventor： Haldor F. A. Topsøe , Hans Jensen-Holm , Ole Ekner , Søren Selde Enevoldsen , Max Thorhauge , Per Morsing
IPC: B01J8/02
CPC classification number: B01J8/0065 , B01D53/885 , B01J8/0453 , B01J8/0492 , B01J2208/00707
Abstract: An up-flow reactor for the catalytic treatment of particle containing gas comprising at least one fixed catalytic bed; at least one drain pipe located upstream of the fixed catalytic bed, the drain pipe disposed within the reactor and a dust rectifier located downstream of the drain pipe and upstream of the fixed catalytic bed.
Abstract translation: 一种用于催化处理包含至少一个固定催化床的含颗粒气体的上流式反应器; 位于固定催化剂床的上游的至少一个排水管，设置在反应器内的排水管，以及位于排水管下游和固定催化床上游的除尘整流器。
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